US4614648A - Process for manufacturing effervescent granules and tablets - Google Patents
Process for manufacturing effervescent granules and tablets Download PDFInfo
- Publication number
- US4614648A US4614648A US06/643,980 US64398084A US4614648A US 4614648 A US4614648 A US 4614648A US 64398084 A US64398084 A US 64398084A US 4614648 A US4614648 A US 4614648A
- Authority
- US
- United States
- Prior art keywords
- solvent
- drying
- mixture
- citric acid
- raw materials
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
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Classifications
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K9/00—Medicinal preparations characterised by special physical form
- A61K9/0002—Galenical forms characterised by the drug release technique; Application systems commanded by energy
- A61K9/0007—Effervescent
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
- B01J2/16—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by suspending the powder material in a gas, e.g. in fluidised beds or as a falling curtain
Definitions
- the present invention relates to an improved process for manufacturing effervescent mixtures and tablets containing in particular active principles for pharmaceutical use.
- this technique presents the drawback of necessitating the transfer of the filler, after step (1), from the mixer to the drier. Consequently, the effervescent reaction triggered off in the mixer cannot be mastered with total precision as its interruption, which occurs in step (2) in the drier, depends on the time for emptying and transferring the filler towards the drier, which time varies from one batch to the following.
- FIG. 1 shows the apparatus, and in particular the granulator-drier, used for the tests referred to hereinbelow according to one variant embodiment of the invention.
- FIG. 2 schematically shows the arrangement of apparatus according to another variant of the invention in a production tower.
- FIG. 1 a granulator-drier operating entirely in fluid bed is used.
- Granulator-driers of the type which will be described hereinafter have been known for a long time.
- This process of granulation also enables mixtures of powders of homogeneous chemical composition to be obtained by using fluidization.
- Granulation consists in a fixation by chemical bond of the particles of sodium bicarbonate and of citric acid. These chemical bonds are obtained by an addition of a defined quantity of demineralized water which provokes a partial effervescent reaction with the formation of mono-, di- or trisodium citrate. These molecules of sodium citrate are considered as bridges bonding the particles of sodium bicarbonate and the particles of citric acid and give the mixture the physical properties of compressibility.
- aqueous solvent water or wetting solution
- the proces of granulation-drying is applicable in particular to the production of an excipient type effervescent mixture on which the active principles and lubricants are added in a subsequent operation; by way of example, we shall cite the parameters defined for buffered effervescent aspirin, for which a wet-process granulation is effected on 3 compounds: sodium bicarbonate, citric acid and possibly glycocoll (binding agent).
- the invention enables a process of production employing a vacuum to be carried out in particularly effective manner. This technique makes it possible:
- a further original feature of the invention resides in the fact that the apparatus have been grouped together in a vertical production tower.
- the process for producing effervescent granules intended for compression is characterized by the creation of a tower 1 in which the following operations are carried out:
- Operations 1 to 6 occur vertically downwardly, transfers taking place by gravity and being dustfree.
- the interest resides in the fact that the 3 operations of point 3 (mixing, granulation, drying) can be automated from the standpoint of monitoring of the process.
- operations 1 to 5 in their chronological sequence may be automated.
- Such automatization renders the process economical from the standpoint of manpower (about 1 t/hr. for 2 persons) by elimination of the interruptions between the operations.
- the apparatus serving for mixing-granulation-drying is composed of a perfectly sealed tank, provided with a system of mechanical stirring for mixing the incorporated powders and equipped with lump-breaking cutters which divide the agglomerates formed by the solvent during wetting.
- This tank must also comprise:
- thermometric probe All the mechanical or physical elements intervening in the successive operations of granulation-drying are monitored by thermometric probe, by measurement of amperage and vacuum.
- an apparatus of the adapted DVT Lodige type is suitable.
- a further originality of the invention resides in the use of a heat exchange hopper for cooling the granules.
- Examples 1 to 4 relate to the first variant, and I and II to the second variant of the invention.
- Air temperature 64° C.
- the solvent is always sprayed on the powders in suspension in air, which makes it possible to increase the exchange surface between the base particles and the acid particles; at this stage of operation, the output and spray time must be monitored.
- the rate of flow of air is to be monitored so as to avoid too great a turbulence of the powders in the cavity of the apparatus, which would render the particles fragile.
- Granulation on granulator-drier of an effervescent mixture containing a plurality of active principles Granulation on granulator-drier of an effervescent mixture containing a plurality of active principles.
- Air temperature 64° C.
- the different raw materials mentioned above are successively incorporated in the mixer 4 without taking into account any physical incompatibilities existing therebetween.
- the premix is effected in 3 minutes. During this period of time, the temperature of the powder is raised by introducing a heat-exchange liquid in the double jacket of the mixer.
- the solvent is a mixture of water/sodium dioctylsulfosuccinate.
- Granulation is effected under atmospheric pressure for 5 minutes.
- This operation lasts about 37 minutes, stoppage of drying being triggered off by monitoring the residual humidity of the powder.
- thermolabile active products not to be destabilized
- the calcium carbasalate will be stored in one of hoppers 2. It will then be pre-weighed at 3 and incorporated in the mixer-granulator-drier 4.
- the automation of the tower makes it possible to eliminate the functions of mixing and granulation and to conserve only the drying function of apparatus 4.
- the auxiliary constituents aroma, PEG and ammonium saccharinate, are added into the band mixer.
Landscapes
- Health & Medical Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Epidemiology (AREA)
- General Health & Medical Sciences (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Veterinary Medicine (AREA)
- Medicinal Chemistry (AREA)
- Pharmacology & Pharmacy (AREA)
- Public Health (AREA)
- Life Sciences & Earth Sciences (AREA)
- Animal Behavior & Ethology (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Preparation (AREA)
- Medical Preparation Storing Or Oral Administration Devices (AREA)
- Glanulating (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Detergent Compositions (AREA)
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR8221476A FR2537872B1 (fr) | 1982-12-21 | 1982-12-21 | Procede de fabrication de comprimes effervescents |
FR8221476 | 1982-12-21 | ||
FR838319143A FR2555439B1 (fr) | 1983-11-30 | 1983-11-30 | Procede et appareillage de fabrication de granules et comprimes effervescents |
FR8319143 | 1983-11-30 |
Publications (1)
Publication Number | Publication Date |
---|---|
US4614648A true US4614648A (en) | 1986-09-30 |
Family
ID=26223202
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US06/643,980 Ceased US4614648A (en) | 1982-12-21 | 1983-12-20 | Process for manufacturing effervescent granules and tablets |
US07/071,991 Expired - Lifetime USRE33086E (en) | 1982-12-21 | 1987-07-10 | Process for manufacturing effervescent granules and tablets and high efficiency granulation tower for such process |
Family Applications After (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US07/071,991 Expired - Lifetime USRE33086E (en) | 1982-12-21 | 1987-07-10 | Process for manufacturing effervescent granules and tablets and high efficiency granulation tower for such process |
Country Status (19)
Country | Link |
---|---|
US (2) | US4614648A (xx) |
EP (1) | EP0162043B1 (xx) |
JP (1) | JPH07100653B2 (xx) |
KR (1) | KR900007312B1 (xx) |
AT (1) | AT394492B (xx) |
CA (1) | CA1209040A (xx) |
CH (1) | CH664491A5 (xx) |
DE (1) | DE3390423C2 (xx) |
DK (1) | DK163565C (xx) |
EG (1) | EG17260A (xx) |
ES (1) | ES528271A0 (xx) |
GB (1) | GB2146244B (xx) |
GR (1) | GR81352B (xx) |
IT (1) | IT1175295B (xx) |
MA (1) | MA19980A1 (xx) |
NL (1) | NL193488C (xx) |
PT (1) | PT77864B (xx) |
SE (1) | SE457416B (xx) |
WO (1) | WO1984002468A1 (xx) |
Cited By (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4762702A (en) * | 1984-11-05 | 1988-08-09 | Gerhard Gergely | Pharmaceutical preparation containing ibuprofen and a process for its preparation |
US4772467A (en) * | 1985-02-19 | 1988-09-20 | Board Of Regents, U T Systems | Osteoporosis inhibition by dietary calcium supplementation |
US4814177A (en) * | 1986-03-18 | 1989-03-21 | Board Of Regents, University Of Texas System | Ultradense and more soluble and bioavailable preparations of calcium citrate |
US4851221A (en) * | 1985-02-19 | 1989-07-25 | Mission Pharmacal Company | Liquid calcium supplementation from readily soluble mixtures of calcium compound and citric acid |
US4859472A (en) * | 1986-12-20 | 1989-08-22 | Boehringer Mannheim Gmbh | Clodronate-containing medicaments and a process for the preparation thereof |
USRE33086E (en) * | 1982-12-21 | 1989-10-10 | Process for manufacturing effervescent granules and tablets and high efficiency granulation tower for such process | |
US4904478A (en) * | 1983-08-11 | 1990-02-27 | Mission Pharmacal Company | Slow-release sodium fluoride tablet and method for treatment of osteoporosis |
US5009809A (en) * | 1989-05-16 | 1991-04-23 | J. M. Huber Corporation | High temperature endothermic blowing agents compositions and applications |
US5009810A (en) * | 1989-05-16 | 1991-04-23 | J. M. Huber Corporation | Endothermic blowing agents compositions and applications |
US5106534A (en) * | 1989-05-16 | 1992-04-21 | J. M. Huber Corporation | Endothermic blowing agents compositions and applications |
US5137655A (en) * | 1989-05-16 | 1992-08-11 | J. M. Huber Corporation | High temperature endothermic blowing agents compositions and applications |
US5250224A (en) * | 1989-05-16 | 1993-10-05 | J. M. Huber Corporation | Foamed products containing endothermic blowing agents and processes |
US5252618A (en) * | 1989-05-16 | 1993-10-12 | J. M. Huber Corporation | Endothermic blowing agents for strengthening weld lines in molded thermoplastic resins and products |
US5252213A (en) * | 1989-06-20 | 1993-10-12 | University Of Washington | Dry dialysate composition |
US5302455A (en) * | 1989-05-16 | 1994-04-12 | J. M. Huber Corporation | Endothermic blowing agents compositions and applications |
US5317044A (en) * | 1989-05-16 | 1994-05-31 | J. M. Huber Corporation | Endothermic blowing agents for surface migration of components in foamed products, compositions and applications |
USRE35368E (en) * | 1989-05-16 | 1996-10-29 | J. M. Huber Corporation | Endothermic blowing agents for surface migration of components in foamed products, compositions and applications |
USRE35447E (en) * | 1989-05-16 | 1997-02-11 | J. M. Huber Corporation | Endothermic blowing agents for strengthening weld lines in molded thermoplastic resins and products |
US5611962A (en) * | 1992-05-13 | 1997-03-18 | Gaia Research | Production of encapsulated chemical foaming concentrates |
WO1999008056A1 (de) * | 1997-08-08 | 1999-02-18 | Glatt Process Technology Gmbh | Verfahren und vorrichtung zum aufarbeiten einer lösung oder feststoffsuspension enthaltend thermisch labile komponenten |
US6602520B1 (en) * | 1999-07-08 | 2003-08-05 | Bayer Ag | Method for producing quickly decomposable solid pharmaceutical preparations |
US6620433B2 (en) | 2000-11-03 | 2003-09-16 | Laboratorios Belmac, S.A. | Dispersible and soluble galenic paracetamol formulation, method for its preparation and its applications |
WO2013081567A1 (en) * | 2011-12-02 | 2013-06-06 | Mahmut Bilgic | Effervescent antipsychotic formulations |
US11219594B2 (en) | 2015-12-12 | 2022-01-11 | Steerlife India Private Limited | Effervescent compositions of metformin and processes for preparation thereof |
US11576855B2 (en) | 2014-09-17 | 2023-02-14 | Steerlife India Private Limited | Effervescent composition and method of making it |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2174004B (en) * | 1985-04-23 | 1988-11-30 | American Cyanamid Co | Pharmaceutical tablet preparations |
IT1209667B (it) * | 1985-11-12 | 1989-08-30 | Zambon Spa | Composizione effeverscente adattivita' analgesica. |
CA2009326C (en) * | 1989-05-09 | 1998-01-27 | Lawrence J. Daher | Aqueous granulation solution and a method of tablet granulation |
US5348745A (en) * | 1989-05-09 | 1994-09-20 | Miles Inc. | Aqueous granulation solution and a method of tablet granulation |
US5298261A (en) * | 1992-04-20 | 1994-03-29 | Oregon Freeze Dry, Inc. | Rapidly distintegrating tablet |
US5503846A (en) * | 1993-03-17 | 1996-04-02 | Cima Labs, Inc. | Base coated acid particles and effervescent formulation incorporating same |
EP0673644A1 (en) * | 1994-03-18 | 1995-09-27 | E-PHARMA TRENTO S.p.A. | Process and plant for preparation of effervescent granules |
FR2796841B1 (fr) * | 1999-07-28 | 2003-08-15 | Lipha | Nouveau procede de production de melanges effervescents et les comprimes qui en resultent |
PT1846147E (pt) * | 2005-02-09 | 2008-10-06 | Satoru Watano | Máquina granuladora e amassadora |
JP5467751B2 (ja) * | 2008-09-29 | 2014-04-09 | 小林製薬株式会社 | タンパク質凝固作用が抑制されてなるアミノ酸含有固体組成物 |
DE102016218135A1 (de) | 2016-09-21 | 2018-03-22 | Robert Bosch Gmbh | Produktionsmodul zum Herstellen fester Arzneiformen |
Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2463962A (en) * | 1947-05-17 | 1949-03-08 | Fearn Lab Inc | Product for producing effervescing carbonated beverages |
US2497057A (en) * | 1950-02-07 | Toilet bowl -gleanee | ||
US2985562A (en) * | 1958-03-27 | 1961-05-23 | Warner Lambert Pharmaceutical | Effervescent compositions |
US2999293A (en) * | 1957-09-12 | 1961-09-12 | Warner Lambert Pharmaceutical | Process of granulating effervescent materials |
US3401216A (en) * | 1964-01-09 | 1968-09-10 | Bristol Myers Co | Methods for preparing pharmaceutical compositions |
US3480185A (en) * | 1966-06-20 | 1969-11-25 | Johnson & Johnson | Charged effervescing agent and medicament dispensing metering valve-actuated aerosol container producing a dose of medicament and carbonation in water |
FR2092893A1 (xx) * | 1970-06-29 | 1972-01-28 | Bru Jean | |
US3773922A (en) * | 1971-04-06 | 1973-11-20 | Fr Dev Rech Sofrader | Method for the manufacture of effervescent tablets |
US3903255A (en) * | 1971-05-17 | 1975-09-02 | Rohm & Haas | Effervescent potassium chloride tablet |
EP0011489A1 (en) * | 1978-11-16 | 1980-05-28 | Beecham Group Plc | An analgesic effervescent powder and process for its preparation |
US4267164A (en) * | 1980-01-31 | 1981-05-12 | Block Drug Company Inc. | Effervescent stannous fluoride tablet |
EP0076340A1 (de) * | 1981-10-06 | 1983-04-13 | Gerhard Dr. Gergely | Verfahren zur Herstellung von gewünschtenfalls zu Brausetabletten verarbeitbaren Brausegranulaten |
Family Cites Families (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1060093B (de) * | 1957-04-26 | 1959-06-25 | Ciba Geigy | Neue Methode zur Herstellung eines Tablettengranulates |
US2877159A (en) * | 1957-04-26 | 1959-03-10 | Ciba Pharm Prod Inc | Method for preparing tablet granulations |
FR2132521A1 (en) * | 1971-04-06 | 1972-11-24 | Sofrader Sa | Effervescent tablets prdn - by controlled drying in effervescent granule formation |
FR2154323A1 (en) * | 1971-09-29 | 1973-05-11 | Sofrader Sa | Effervescent tablets prdn - by controlled drying in effervescent granule formation |
DE2218729B1 (de) * | 1972-04-18 | 1974-03-21 | Barmag Barmer Maschinenfabrik Ag, 5600 Wuppertal | Vorrichtung zum mischen und granulieren |
US4093710A (en) * | 1976-07-07 | 1978-06-06 | Sandoz, Inc. | Rapid dissolving effervescent granules |
US4153678A (en) * | 1978-07-17 | 1979-05-08 | American Cyanamid Company | Levamisole effervescent tablets |
DE2842822C3 (de) * | 1978-09-30 | 1982-05-19 | Merz + Co GmbH & Co, 6000 Frankfurt | Arzneistoffzubereitungen schwerlöslicher Arzneistoffe in Form von Brausegranulaten |
AT372299B (de) * | 1980-12-15 | 1983-09-26 | Gergely Gerhard | Vorrichtung zur herstellung von gewuenschtenfalls zu brausetabletten verarbeitbaren brausegranulaten |
CA1209040A (fr) * | 1982-12-21 | 1986-08-05 | Jean Bru | Procede de fabrication de granules et comprimes effervescents |
-
1983
- 1983-12-19 CA CA000443701A patent/CA1209040A/fr not_active Expired
- 1983-12-20 US US06/643,980 patent/US4614648A/en not_active Ceased
- 1983-12-20 GB GB08427318A patent/GB2146244B/en not_active Expired
- 1983-12-20 CH CH4062/84A patent/CH664491A5/fr not_active IP Right Cessation
- 1983-12-20 PT PT77864A patent/PT77864B/pt unknown
- 1983-12-20 DE DE3390423T patent/DE3390423C2/de not_active Expired - Lifetime
- 1983-12-20 WO PCT/FR1983/000253 patent/WO1984002468A1/fr active IP Right Grant
- 1983-12-20 AT AT0908083A patent/AT394492B/de not_active IP Right Cessation
- 1983-12-20 EP EP84900064A patent/EP0162043B1/fr not_active Expired
- 1983-12-20 JP JP59500291A patent/JPH07100653B2/ja not_active Expired - Lifetime
- 1983-12-20 NL NL8320404A patent/NL193488C/nl not_active IP Right Cessation
- 1983-12-20 GR GR73291A patent/GR81352B/el unknown
- 1983-12-21 EG EG79483A patent/EG17260A/xx active
- 1983-12-21 IT IT68331/83A patent/IT1175295B/it active
- 1983-12-21 KR KR1019830006082A patent/KR900007312B1/ko not_active IP Right Cessation
- 1983-12-21 ES ES528271A patent/ES528271A0/es active Granted
- 1983-12-21 MA MA20201A patent/MA19980A1/fr unknown
-
1984
- 1984-08-20 SE SE8404142A patent/SE457416B/sv not_active IP Right Cessation
- 1984-08-20 DK DK397984A patent/DK163565C/da not_active IP Right Cessation
-
1987
- 1987-07-10 US US07/071,991 patent/USRE33086E/en not_active Expired - Lifetime
Patent Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2497057A (en) * | 1950-02-07 | Toilet bowl -gleanee | ||
US2463962A (en) * | 1947-05-17 | 1949-03-08 | Fearn Lab Inc | Product for producing effervescing carbonated beverages |
US2999293A (en) * | 1957-09-12 | 1961-09-12 | Warner Lambert Pharmaceutical | Process of granulating effervescent materials |
US2985562A (en) * | 1958-03-27 | 1961-05-23 | Warner Lambert Pharmaceutical | Effervescent compositions |
US3401216A (en) * | 1964-01-09 | 1968-09-10 | Bristol Myers Co | Methods for preparing pharmaceutical compositions |
US3480185A (en) * | 1966-06-20 | 1969-11-25 | Johnson & Johnson | Charged effervescing agent and medicament dispensing metering valve-actuated aerosol container producing a dose of medicament and carbonation in water |
FR2092893A1 (xx) * | 1970-06-29 | 1972-01-28 | Bru Jean | |
US3773922A (en) * | 1971-04-06 | 1973-11-20 | Fr Dev Rech Sofrader | Method for the manufacture of effervescent tablets |
US3903255A (en) * | 1971-05-17 | 1975-09-02 | Rohm & Haas | Effervescent potassium chloride tablet |
EP0011489A1 (en) * | 1978-11-16 | 1980-05-28 | Beecham Group Plc | An analgesic effervescent powder and process for its preparation |
US4267164A (en) * | 1980-01-31 | 1981-05-12 | Block Drug Company Inc. | Effervescent stannous fluoride tablet |
EP0076340A1 (de) * | 1981-10-06 | 1983-04-13 | Gerhard Dr. Gergely | Verfahren zur Herstellung von gewünschtenfalls zu Brausetabletten verarbeitbaren Brausegranulaten |
Cited By (29)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
USRE33086E (en) * | 1982-12-21 | 1989-10-10 | Process for manufacturing effervescent granules and tablets and high efficiency granulation tower for such process | |
US4904478A (en) * | 1983-08-11 | 1990-02-27 | Mission Pharmacal Company | Slow-release sodium fluoride tablet and method for treatment of osteoporosis |
US4762702A (en) * | 1984-11-05 | 1988-08-09 | Gerhard Gergely | Pharmaceutical preparation containing ibuprofen and a process for its preparation |
US4772467A (en) * | 1985-02-19 | 1988-09-20 | Board Of Regents, U T Systems | Osteoporosis inhibition by dietary calcium supplementation |
US4851221A (en) * | 1985-02-19 | 1989-07-25 | Mission Pharmacal Company | Liquid calcium supplementation from readily soluble mixtures of calcium compound and citric acid |
US4814177A (en) * | 1986-03-18 | 1989-03-21 | Board Of Regents, University Of Texas System | Ultradense and more soluble and bioavailable preparations of calcium citrate |
US4859472A (en) * | 1986-12-20 | 1989-08-22 | Boehringer Mannheim Gmbh | Clodronate-containing medicaments and a process for the preparation thereof |
US5252618A (en) * | 1989-05-16 | 1993-10-12 | J. M. Huber Corporation | Endothermic blowing agents for strengthening weld lines in molded thermoplastic resins and products |
USRE35239E (en) * | 1989-05-16 | 1996-05-14 | J.M. Huber Corporation | Endothermic blowing agents compositions and applications |
US5037580A (en) * | 1989-05-16 | 1991-08-06 | J. M. Huber Corporation | Endothermic blowing agents for strengthening weld lines in molded thermoplastic resins and products |
US5045570A (en) * | 1989-05-16 | 1991-09-03 | J. M. Huber Corporation | Endothermic blowing agents for surface migration of components in foamed products, compositions and applications |
US5106534A (en) * | 1989-05-16 | 1992-04-21 | J. M. Huber Corporation | Endothermic blowing agents compositions and applications |
US5137655A (en) * | 1989-05-16 | 1992-08-11 | J. M. Huber Corporation | High temperature endothermic blowing agents compositions and applications |
US5250224A (en) * | 1989-05-16 | 1993-10-05 | J. M. Huber Corporation | Foamed products containing endothermic blowing agents and processes |
US5009809A (en) * | 1989-05-16 | 1991-04-23 | J. M. Huber Corporation | High temperature endothermic blowing agents compositions and applications |
USRE35447E (en) * | 1989-05-16 | 1997-02-11 | J. M. Huber Corporation | Endothermic blowing agents for strengthening weld lines in molded thermoplastic resins and products |
US5302455A (en) * | 1989-05-16 | 1994-04-12 | J. M. Huber Corporation | Endothermic blowing agents compositions and applications |
US5317044A (en) * | 1989-05-16 | 1994-05-31 | J. M. Huber Corporation | Endothermic blowing agents for surface migration of components in foamed products, compositions and applications |
US5009810A (en) * | 1989-05-16 | 1991-04-23 | J. M. Huber Corporation | Endothermic blowing agents compositions and applications |
USRE35368E (en) * | 1989-05-16 | 1996-10-29 | J. M. Huber Corporation | Endothermic blowing agents for surface migration of components in foamed products, compositions and applications |
US5252213A (en) * | 1989-06-20 | 1993-10-12 | University Of Washington | Dry dialysate composition |
US5611962A (en) * | 1992-05-13 | 1997-03-18 | Gaia Research | Production of encapsulated chemical foaming concentrates |
WO1999008056A1 (de) * | 1997-08-08 | 1999-02-18 | Glatt Process Technology Gmbh | Verfahren und vorrichtung zum aufarbeiten einer lösung oder feststoffsuspension enthaltend thermisch labile komponenten |
US6602520B1 (en) * | 1999-07-08 | 2003-08-05 | Bayer Ag | Method for producing quickly decomposable solid pharmaceutical preparations |
US7208175B2 (en) | 1999-07-08 | 2007-04-24 | Bayer Ag | Process for the production of rapidly disintegrating, solid pharmaceutical preparations |
US6620433B2 (en) | 2000-11-03 | 2003-09-16 | Laboratorios Belmac, S.A. | Dispersible and soluble galenic paracetamol formulation, method for its preparation and its applications |
WO2013081567A1 (en) * | 2011-12-02 | 2013-06-06 | Mahmut Bilgic | Effervescent antipsychotic formulations |
US11576855B2 (en) | 2014-09-17 | 2023-02-14 | Steerlife India Private Limited | Effervescent composition and method of making it |
US11219594B2 (en) | 2015-12-12 | 2022-01-11 | Steerlife India Private Limited | Effervescent compositions of metformin and processes for preparation thereof |
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